Production technology of nitroguanidine
A production process and technology for nitroguanidine, applied in the field of nitroguanidine production technology, can solve the problems of large amount of waste acid and low content of crude nitroguanidine, and achieve the effect of no three wastes
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Embodiment 1
[0013] Add 1000Kg concentrated sulfuric acid into a 2000-liter enamel reaction kettle, stir the solution at a speed of 68-69r / min, the reaction kettle is jacketed, and -10°C cooling brine is passed inside, and the content of 90% is slowly added to the reaction kettle 500Kg of guanidine nitrate, the feed rate of guanidine nitrate is based on the temperature of the reaction solution being controlled between 30-40°C. After the feeding is completed, the dehydration reaction is carried out at 39-41°C for 1 hour, and the dehydration reaction ends;
[0014] Add 4000 liters of water into the hydrolysis reaction kettle, control the water temperature between 5-10°C, stir at a speed of 68-69r / min, then add the above dehydration reaction solution, the addition speed of the dehydration reaction solution is to control the temperature of the hydrolyzate not to exceed 30 ℃ as the benchmark, after the addition is completed, the hydrolysis reaction is carried out at a temperature of 20-30 ℃ for ...
Embodiment 2
[0017] The steps described in Example 1, the difference is that the quality of concentrated sulfuric acid is 1100Kg, and the final obtained hydrous nitroguanidine crude product has a loss on drying: 26% (water), content: 97.9% (HPLC), weight: 514 Kg, molar yield: 97.1%.
Embodiment 3
[0019] Describe the steps with Example 1, the difference is that the volume of water added in the hydrolysis reactor is 3000 liters, and finally obtain the crude product of hydrous nitroguanidine, its loss on drying: 25% (water), content: 97.5% (HPLC), Weight: 513 Kg, molar yield: 97.8%.
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